Method and composition for removing resist, etch residue, and copper oxide from substrates having copper, metal hardmask and low-k dielectric material

ABSTRACT

A semiconductor processing composition and method for removing photoresist, polymeric materials, etching residues and copper oxide from a substrate comprising copper, low-k dielectric material and TiN, TiNxOy or W wherein the composition includes water, at least one halide anion selected from Cl −  or Br − , and, where the metal hard mask comprises only TiN or TiNxOy, optionally at least one hydroxide source.

INCORPORATION BY REFERENCE

The entirety of U.S. patent application Ser. No. 13/209,859, filed on Aug. 15, 2011, is hereby expressly incorporated herein by reference.

BACKGROUND OF THE INVENTION

The presently disclosed and claimed inventive concept(s) relates to compositions and methods for cleaning integrated circuit substrates, and, more particularly, to compositions and methods comprising a halide anion which are effective in removing photoresist, post etch residue, and/or post planarization residue from substrates comprising copper, low-k dielectric material and metal hardmask, such as TiN, TiNxOy and W.

Devices with critical dimensions on the order of 90 nanometers (nm) have involved integration of copper conductors and low-k dielectrics, and they require alternating material deposition processes and planarization processes. As the technology nodes advance to 45 nm and smaller, the decreasing size of semiconductor devices makes achieving critical profile control of vies and trenches more challenging. Integrated circuit device companies are investigating the use of metal hardmasks to improve etch selectivity to low-k materials and thereby gain better profile control.

In order to obtain high yield and low resistance interconnects, the polymers on the sidewalls and the particulate/polymer residues at the via bottoms that are generated during etching must be removed prior to the next process step. It would be very beneficial if the cleaning solution can also effectively etch the selected hardmask to form an intermediate morphology, e.g., a pulled-back/rounded morphology. A pulled-back/rounded morphology could prevent undercutting the hardmask, which, in turn, could enable reliable deposition of barrier metal, Cu seed layer and Cu filling. Alternatively, fully removing the metal hardmask using the same composition could offer numerous benefits to downstream process steps, particularly chemical mechanical polishing (CMP), by eliminating a need for barrier CMP.

Following almost every step in the fabrication process, e.g., a planarization step, a trenching step, or an etching step, cleaning processes are required to remove residues of the plasma etch, oxidizer, abrasive, metal and/or other liquids or particles that remain and which can contaminate the surface of the device if not effectively removed. Fabrication of advanced generation devices that require copper conductors and low-k dielectric materials (typically carbon-silica or porous silica materials), give rise to the problem that both materials can react with and be damaged by various classes of prior art cleaners.

Low-k dielectrics, in particular, may be damaged in the cleaning process as evidenced by etching, changes in porosity/size, and ultimately changes in dielectric properties. Time required to remove residues depends on the nature of the residue, the process (heating, crosslinking, etching, baking, and/or ashing) by which it is created, and whether batch or single wafer cleaning processes are used. Some residues may be cleaned in a very short period of time, while some residues require much longer cleaning processes. Compatibility with both the low-k dielectric and with the copper conductor over the duration of contact with the cleaner is a desired characteristic.

When TiN, TiNxOy or W is used as an etching hard mask to gain high selectivity to low-k materials during a dry etching process in processing advanced copper/low-k semiconductor devices, effective cleaning compositions that can selectively etch TiN, TiNxOy or W must not only be compatible with copper and the low-k materials, but must also be effective in simultaneously removing polymeric materials and etch residues.

With the continuing reduction in device critical dimensions and continuing needs for production efficiency and device performance, there is a need for improved cleaning compositions.

SUMMARY OF THE INVENTION

The presently claimed and disclosed inventive concept(s) relate to an improved semiconductor processing composition, i.e., a wet cleaning formulation, for removing photoresist, polymeric materials, etching residues and copper oxide from substrates wherein the substrate comprises copper, a low-k dielectric material(s) and metal hard mask selected from TiN, TiNxOy or W. The composition comprises water, at least one halide anion selected from Cl⁻ or Br⁻, and at least one oxidizing agent. Although not required for carrying out the invention, at least one Cu corrosion inhibitor may also be present in the composition where the composition is to be deployed in semiconductor processing at FEOL applications and other applications where corrosion of Cu components is not a concern. In cases where the metal hard mask is TiN or TiNxOy, the composition in one embodiment will also include a base, i.e., hydroxide source, as appropriate to maintain the pH of the composition at a value of at least 7 or above for best results.

In some cases where the metal hard mask is TIN or TiNxOy, the composition in an alternate embodiment may have a pH at a value of less than 7, and even as low as 4.6, and achieve satisfactory results.

In cases where the metal hard mask is W, the pH working range according to yet another embodiment can be basic or acidic and achieve satisfactory results.

The oxidizing agent is selected from the group consisting of hydrogen peroxide, ozone, ferric chloride, permanganate, peroxoborate, perchlorate, persulfate, ammonium peroxydisulfate, per acetic acid, urea hydroperoxide, percarbonate, perborate, and mixtures thereof. When present, the Cu corrosion inhibitor is selected from the group consisting of a heterocyclic compound which contains a nitrogen atom in the form of ═N— as a ring form member. The heterocyclic compound can be used singly or the Cu corrosion inhibitor can comprise a mixture of such heterocyclic compounds. In addition, mercaptan, thiourea, aromatic hydrazides, Schiff bases, indoles and derivatives thereof may also produce satisfactory results in inhibiting Cu corrosion.

In another embodiment the invention comprises a method for simultaneously removing one or more of photoresist, polymeric materials, etching residues and copper oxide from a substrate comprising copper, low-k dielectric material and TiN, TiNxOy or W. The method comprises applying to the substrate an aqueous composition consisting essentially of at least one halide anion selected from Cl⁻ or Br⁻, at least one oxidizing agent selected from the group set forth above, and optionally at least one Cu corrosion inhibitor selected from the group set forth above. In cases where the metal hard mask is TiN or TiNxOy, the composition may also include a base, i.e., hydroxide source, as appropriate to maintain the pH of the composition at a value of at least 7 or above for best results. In some cases where the metal hard mask is TiN or TiNxOy, the composition in an alternate embodiment may have a pH at a value of less than 7, and even as low as 4.6, and achieve satisfactory results. In cases where the metal hard mask is W, the pH working range can be basic or acidic and achieve satisfactory results. The amount of undesirable residue to be removed in any given processing step will influence the selection of operating pH value for the composition.

The compositions and method according to the inventive concepts described herein are uniquely capable of selectively etching TiN, TiNxOy or W, are compatible with Cu and low-k dielectric materials, and can also simultaneously remove copper oxides, polymeric materials and etch residues from the substrate being treated. A composition formulated according to the invention and exhibiting an inherently high etch rate for TiN, TiNxOy or W enables processing at low temperature, e.g., temperatures less than 65° C. A relatively low temperature process exhibits a reduced oxidizer decomposition rate, which, in turn, extends the useful composition bath life. Additionally, compositions according to the invention which exhibit high TiN, TiNxOy or W etch rates are desirable because they can reduce device processing time and thereby increase device throughput. Typically, high TiN, TiNxOy or W etch rates have been accomplished by increasing process temperatures. However, for single wafer process applications, the highest processing temperature is around 65° C., which, in turn, can limit the upper end of TiN etch rates, and thereby limit complete removal of the TiN metal hardmask. Compositions according to the invention can effectively deliver high etch rates for TiN, TiNxOy or W with single wafer tool applications in a temperature range of from 20° C. to 60° C., and the TiN, TiNxOy or W metal hardmask can be fully removed with single wafer application process equipment if so desired.

BRIEF DESCRIPTION OF THE DRAWINGS

FIGS. 1A to 1C are cross-sectional diagrams of a semiconductor device as received and during and after processing according to the inventive concepts.

FIGS. 2 and 3 are graphs of metal hard mask etch rate vs. concentration of halide anion at pH 8.7 and 30° C.

FIGS. 4 and 5 are graphs of metal hard mask etch rate vs. concentration of halide anion at pH 7 and 30° C.

FIGS. 6 and 7 are graphs of metal hard mask etch rate vs. concentration of halide anion at pH 8.7 and 20° C.

FIGS. 8 and 9 are graphs of metal hard mask etch rate vs. concentration of halide anion at pH 8.7 and 55° C.

FIGS. 10A to 10I are SEM images of TiN metal hardmask removal using a composition according to the invention.

FIGS. 11 to 14 are graphs of W metal hardmask etch rate at 30° C. and pH values of 3.4 and 8.7.

FIG. 15 is a graph of TEOS etch rate vs. NH₄Cl, NH₄Br, and NH₄F at 30° C. and pH 7.

FIG. 16 is a graph of TEOS etch rate vs. NH₄Cl, NH₄Br, and NH₄F at 50° C. and pH 7.

FIGS. 17A to 17D are SEM images of cleaning results for wafers as received and after processing with a composition according to the invention.

FIG. 18 is a graph of TEOS etch rate vs. NH₄F and NH₄Br at 55° C. and pH 7.

FIG. 19 is a graph of TEOS etch rate vs. NH₄F and NH₄Br at 55° C. and pH 8.

FIG. 20 is a graph of TEOS etch rate vs. NH₄F and NH₄Cl at 55° C. and pH 7.

FIG. 21 is a graph of TEOS etch rate vs. NH₄F and NH₄Cl at 55° C. and pH 8.

FIG. 22 is a graph of TN etch rate vs. NH₄Br at 40° C. and pH 8.

FIG. 23 is a graph of TIN etch rate vs. NH₄Cl at 40° C. and pH 8.

DETAILED DESCRIPTION OF THE INVENTION

It is recognized that various components of the compositions of this invention may interact, and, therefore, any composition is expressed as the amount of various components which, when added together, form the composition. Unless specifically stated otherwise, any composition given in percent is percent by weight of that component that has been added to the composition. When the composition is described as being substantially free of a particular component, generally there are numeric ranges provided to guide one of ordinary skill in the art to what is meant by “substantially free,” but in all cases “substantially free” encompasses the preferred embodiment where the composition is totally free of that particular component.

According to a first embodiment, the present invention is a semiconductor processing composition comprising water, at least one halide anion selected from Cl⁻ or Br⁻, at least one oxidizing agent, and optionally at least one hydroxide source depending on the desired pH for the composition. Although not required for carrying out the invention, at least one Cu corrosion inhibitor may also be present in the composition where the composition is to be deployed in semiconductor processing at FEOL applications and other applications where corrosion of Cu components is not a concern. In one embodiment, the formulations preferably have a pH of from 7.0 and higher for removing hardmasks comprising TiN and TiNxOy. As pointed out above, in some applications the formulations can produce satisfactory results when the pH is below 7. For removing hardmask comprising W, the composition comprises water, at least one halide anion selected from Cl⁻ or Br⁻, at least one oxidizing agent, and the pH value can range from acidic to basic. At least one Cu corrosion inhibitor may also be present. The compositions of the invention are effective in simultaneously removing pholoresist, polymeric materials, etching residues and copper oxide from a substrate which includes copper, low-k dielectric material and a metal hardmask selected from TiN, TiNxOy or W. The cleaning composition can effectively etch the metal hardmask to form an intermediate morphology, e.g., a pulled-back/rounded morphology, as shown diagrammatically in FIG. 1B. However, the composition is also capable of fully removing the metal hardmask as shown diagrammatically in FIG. 1C.

FIG. 1A is a cross sectional diagram of a semiconductor device which shows copper conductor 10 in relationship to low-k dielectric material 11, metal hardmask 12, and an interlayer insulating film 13. The interlayer insulating film will typically be p-TEOS (Tetra Ethyl Ortho Silicate) film or SiON (depending on the source). Etch residue, polymer, photoresist 14 remains after a typical processing step in device fabrication.

The compositions and method according to the inventive concepts described herein are uniquely capable of selectively etching metal hard mask, e.g., TiN, TiNxOy and W, whereby the metal hardmask is only partially removed to form a pullback corner rounding scheme 15 as shown in FIG. 1B. An intermediate pullback corner rounding scheme is important because it can prevent undercutting of the hardmask, thus enabling reliable deposition of barrier metal, Cu seed layer, and Cu filling. Alternatively, the metal hardmask can be completely removed as shown in FIG. 1C. Complete removal of the hardmask eliminates the need for barrier CMP and subsequent post-CMP cleaning steps and thereby improves device fabrication yields.

The compositions and method according to the inventive concepts described herein are particularly applicable for processing single waters in single wafer equipment wherein a higher processing temperature in the range of 75° C. is desirable. However, higher temperatures are known to contribute to degradation of the oxidizing agent which shortens bath life. It has been observed according to the inventive concepts described herein that satisfactory results can be achieved in processing multiple wafers at substantially lower temperatures in the range of from 20° C. to 60° C. to generate a TiN pullback scheme or to completely remove TiN metal hardmask.

Cosolvent

In some embodiments of this invention, the composition can contain a cosolvent that is miscible with water. Suitable cosolvents include, but are not limited to, sulfolane, N-methylpyrrolidone, and dimethylsulfoxide.

Oxidizing Agent

Oxidizing agents useful according to the inventive concept(s) are selected from any substance which removes metal electrons and raises the atomic valence and includes, but is notlimited to the group consisting of hydrogen peroxide (H₂O₂), ozone, ferric chloride, permanganate peroxoborate, perchlorate, persulfate, ammonium peroxydisulfate, per acetic acid, urea hydroperoxide, nitric acid (HNO₃), ammonium chlorite (NH₄ClO₂), ammonium chlorate (NH₄ClO₃), ammonium odate (NH₄IO₃), ammonium perborate (NH₄BO₃), ammonium perchlorate (NH₄ClO₄), ammonium periodate (NH₄IO₃), ammonium persulfate ((NH₄)₂S₂O₈), tetramethylammonium chlorite ((N(CH₃)₄)ClO₂), tetramethylammionium chlorate ((N(CH₃)₄)ClO₃), tetramethylammonium iodate ((N(CH₃)₄)IO₃), tetramethylammonium perborate ((N(CH₃)₄)BO₃), tetramethylammonium perchlorate ((N(CH₃)₄)ClO₄), tetramethylammonium periodate ((N(CH₃)₄)IO₄), tetramethylammonium persulfate ((N(CH₃)₄)S₂O₈), ((CO(NH₂)₂)H₂O₂), peracetic acid (CH₃(CO)OOH), and mixtures thereof. Among the foregoing, H₂O₂ is a most preferred oxidizing agent being free of metals and provides ease of handling and lower relative cost.

The oxidizing agent or mixture thereof may be present in the composition at from about 0.0001 wt % to about 95 wt %, and preferably, for best results, at from about 1 wt % to about 80 wt %.

Cu Corrosion Inhibitor

A Cu corrosion inhibitor is an optional component in the composition of this invention. A copper corrosion inhibitor will usually be present in the inventive composition and associated process when used for BEOL (back end of line) applications, where the presence of a corrosion inhibitor is needed to protect copper surfaces from being etched or otherwise degraded. For other applications, including FEOL (Front End Of Line) applications, of the inventive composition and associated method, a corrosion inhibitor is not generally needed, i.e., slight etching/degradation of copper surfaces is not usually a concern, and a corrosion inhibitor is not present in the composition.

Cu Corrosion inhibitors are typically selected from the group consisting of a heterocyclic compound containing a nitrogen atom in the form of ═N— as a ring form member, such as pyrrole and derivatives thereof, pyrazole and derivatives thereof, Imidazole and derivatives thereof, triazole and derivatives thereof, indazole and derivatives thereof and thiol-triazole and derivatives thereof, benzotriazole, tolyltriazole, 5-phenyl-benzotriazole, 5-nitro-benzotriazole, 3-amino-5-mercapto-1,2,4-triazole, 1-amino-1,2,4-triazole, hydroxybenzotriazole, 2-(5-amino-pentyl)-benzotriazole, 1-amino-1,2,3-triazole, 1-amino-5-methyl-1,2,3-triazole, 3-amino-1,2,4-triazole, 3-mercapto-1,2,4-triazole, 3-isopropyl-1,2,4-triazole, 5-phenylthiol-benzotriazole, halo-benzotriazoles (halo=F, Cl, Br or I), naphthotriazole, 2-mercaptobenzimidazole (MBI), 2-mercaptobenzothiazole, 4-methyl-2-phenylimidazole, 2-mercaptothiazoline, 5-aminotetrazole, 5-aminotetrazole monohydrate, 5-amino-1,3,4-thiadiazole-2-thiol, 2,4-diamino-6-methy-1,3,5-triazine, thiazole, triazine, methyltetrazole, 1,3-dimethyl-2-imidazolidinone, 1,5-pentamethylenetetrazole, 1-phenyl-5-mercaptotetrazole, diaminomethyltriazine, imidazoline thione, mercaptobenzimidazole, 4-methyl-4H-1,2,4-triazole-3-thiol, 5-amino-1,3,4-thiadiazole-2-thiol, benzothiazole, and mixtures thereof. Among the foregoing, pyrazole is a preferred Cu corrosion inhibitor for ease of handling and lower relative cost.

Other suitable Cu corrosion inhibitors include, but are not limited to indole, aromatic hydrazides and Schiff base compounds.

The Cu corrosion inhibitor or mixture thereof may be present in the composition at from about 0.0001 wt % to about 30 wt %, and preferably, for best results, at from about 0.01 wt % to about 10 wt %.

Halide Anion

The halide anion component may be selected from any chemical compounds which are capable of generating Cl⁻ and Br⁻ anions, such as NH₄Cl, NH₄Br, quatemary ammonium bromide, NR₄ ⁽⁺⁾Br⁽⁻⁾, or quaternary ammonium chloride, NR₄ ⁽⁺⁾Cl⁽⁻⁾, R being an alkyl group or an aryl group. Preferred compounds include, but are not limited to, NH₄Cl and NH₄Br.

The halide anion may be present in the composition at concentrations of from about 0.001 wt % to about 20 wt %. Best results have been observed when the halide anion is present in the composition in a range of from about 0.05 wt % to about 5 wt %.

EXAMPLES

Compositions according to the invention are now explained in detail by reference to the inventive concepts and comparative examples which follow, but the present invention is not limited by these examples.

The compositions shown in Tables 1A & 1B and in Table 6A, 6B & 6C were prepared using water as the solvent, pyrazole as the Cu corrosion inhibitor, H₂O₂ as the oxidizing agent, and diglycolamine (DGA) as a base to adjust pH. (Water levels in the composition tables below are designated as “DI balance”, which means that water is present at a level such that the weight percent of all components, including water, is equal to 100 weight percent.) The compositions shown in Table 5A were prepared using water as the solvent, pyrazole as Cu corrosion inhibitor, H₂O₂ as the oxidizing agent, and glycolic acid (GA) to adjust pH. Composition pH can generally be adjusted using any suitable acid or base (i.e., proton source for acidic formulation or hydroxide source for basic formulation) which does not adversely affect the semiconductor device being treated, TiN and Cu etch rate evaluations were carried out for ten minutes at 20° C., ten minutes at 30° C. and 40° C., and five minutes at 55° C. in the pH range from 7.0-9.0. TiN and Cu thicknesses were measured using a Four Dimensions Four Point Probe Meter 333A, whereby the resistivity of the film was correlated to the thickness of the film remaining. The etch rate was calculated as the thickness change (before and after chemical treatment) divided by the chemical treatment time. Chemical solution pH was measured with a Beckman 260 pH/Temp/mV meter. The H₂O₂ used in these experiments was semiconductor grade PURANAL (Aldrich 40267). Residue removal performance experiments were conducted at 30° C. for 90 seconds, and the residue removal efficiency and TiN pullback were evaluated from SEM results (Hitachi 5-5500). TEOS etch rate experiments were conducted at 30° C., 50′C and at 55′C for 30 minutes, respectively. The TEOS thickness was measured with Horiba JoBin Yvon Auto SE Spectroscopic Ellipsometer. TEOS etch rate was calculated as the thickness change (before and after chemical treatment) divided by the chemical treatment time.

TiN and Cu Etch Rate

The formulations shown in Table 1A & 1B were prepared and TiN and Cu etch rate evaluations were carried out as described above at a temperature of 30° C.

TABLE 1A Formulations and their pH Component Formulation NH4Br (10%) NH4Cl (10%) Pyrazole DGA (10%) DI balance H2O2 (30%) pH HCX-T002C-32- 0 0 0.5 0.9106 80 20 8.7 Br0-P8 HCX-T002C-32- 0.5 0 0.5 1.1345 80 20 8.7 Br005-P8 HCX-T002C-32- 3 0 0.5 1.7490 80 20 8.7 Br03-P8 HCX-T002C-32- 0 0.5 0.5 1.0970 80 20 8.7 Cl005-P8 HCX-T002C-32- 0 3 0.5 2.2280 80 20 8.7 Cl03-P8

TABLE 1B Formulations and their pH Component Formulation NH4Br (10%) NH4Cl (10%) Pyrazole DGA (10%) DI balance H2O2 (30%) pH HCX-T002C-32- 0 0 0.5 0.0386 80 20 7.0 Br0-P7 HCX-T002C-32- 0.5 0 0.5 0.0520 80 20 7.0 Br005-P7 HCX-T002C-32- 3 0 0.5 0.0801 80 20 7.0 Br03-P7 HCX-T002C-32- 0 0.5 0.5 0.0383 80 20 7.1 Cl005-P7 HCX-T002C-32- 0 3 0.5 0.0440 80 20 6.9 Cl03-P7

TABLE 2 TiN and Cu Etch Rate for Various Formulations at 30° C. Process Temp Formulation (° C.) TiN (Å/min) Cu (Å/min) HCX-T002C-32-P8 30 19.05 0.32 HCX-T002C-32-Br005-P8 31.39 0.61 HCX-T002C-32-Br03-P8 40.53 0.58 HCX-T002C-32-Cl005-P8 34.42 0.51 HCX-T002C-32-Cl03-P8 47.03 1.05 HCX-T002C-32-P7 2.74 −0.23 HCX-T002C-32-Br005-P7 6.92 0.15 HCX-T002C-32-Br03-P7 11.14 −0.26 HCX-T002C-32-Cl005-P7 9.56 0.20 HCX-T002C-32-Cl03-P7 12.90 0.18

The TiN etch rate results at 30° C. are shown graphically in FIGS. 2,3, 4 and 5 where it can be seen that for NH₄Cl and NH₄Br the etch rate for TN metal hardmask increases as the concentration of halide anion increases from 0 to 0.3 wt %; and low Cu etch rates in Table 2 demonstrate that the chemical components of the composition are compatible with Cu.

TiN and Cu etch rate evaluations were carried out as described above at a temperature of 20° C.

TABLE 3 TiN and Cu Etch Rate for Various Formulations at 20° C. Process Formulation Temp (° C.) TiN (Å/min) Cu (Å/min) HCX-T002C-32-P8 20 2.96 0.07 HCX-T002C-32-Br005-P8 7.57 0.01 HCX-T002C-32-Br03-P8 16.14 0.24 HCX-T002C-32-Cl005-P8 9.07 0.05 HCX-T002C-32-Cl03-P8 16.06 0.37

The TiN etch rate results at 20° C. are shown graphically in FIGS. 6 and 7 where it can be seen that for NH₄Cl and NH₄Br the etch rate for TiN metal hardmask increases as the concentration of halide anion increases from 0 to 0.3 wt %, and the low Cu etch rates in Table 3 show that the chemical components of the composition are compatible with Cu.

TiN and Cu etch rate evaluations were carried out as described above at a temperature of 55° C.

TABLE 4 TiN and Cu Etch Rate for Various Formulations at 55° C. Process Formulation Temp (° C.) TiN (Å/min) Cu (Å/min) HCX-T002C-32-P8 55 108.88 1.29 HCX-T002C-32-Br005-P8 120.45 0.66 HCX-T002C-32-Br03-P8 140.87 0.82 HCX-T002C-32-Cl005-P8 136.47 2.40 HCX-T002C-32-Cl03-P8 145.03 5.46

The TIN etch rate at 55° C. results are shown graphically in FIGS. 8 and 9 where it can be seen that for NH₄Cl and NH₄Br the etch rate for TiN metal hardmask increases as the concentration of halide anion increases from a value of 0 to 0.3 wt %, and the low Cu etch rates in Table 4 indicate that the chemical components in the composition are compatible with Cu

SEM pictures of TiN removal are shown in FIG. 10. The TiN hardmask pullback becomes more pronounced as the NH₄Br (or NH₄Cl) concentration is increased from 0 to 0.05% (NH₄Br shown in FIG. 10A and FIG. 10B, and NH₄Cl shown in FIG. 10A and FIG. 10E), and TiN is completely removed with a 0.3 wt % NH₄Br (or NH₄Cl) formulation at 40° C. (FIG. 10C and FIG. 10F). In the absence of NH₄Br (or NH₄Cl), when the process temperature is increased from 40° C. to 50° C., the TiN pullback becomes more significant (FIG. 10A to FIG. 10G). Complete TiN removal is achieved with a 0.3% NH₄Br (or NH₄Cl) formulation at 40° C. (FIG. 10C and FIG. 10F), and with 0.05% NH₄Br (or NH₄Cl) at 50° C. (FIG. 10H and FIG. 10I). The results indicate that to achieve a fixed TIN etch rate (i.e., to form a specific TiN pullback morphology), a formulation containing NH₄Br (or NH₄Cl) requires a much lower process temperature compared with a formulation without NH₄Br (or NH₄Cl), and the TiN etch rate increases with increasing NH₄Br (or NH₄Cl) concentration. The addition of NH₄Br (or NH₄Cl) makes possible the complete removal of TIN metal hard mask with single wafer application process equipment.

W Etch Rate

The formulations shown in Table 1 and Table 5A & 5B were prepared, and W etch rate evaluations were carried out as described above at 30° C.

TABLE 5A Formulations and W etch rate at 30° C., pH 3 W Etch Rate Component (Å/min) at Formulation Pyrazole NH4Br (10%) NH4Cl (10%) H2O2 (30%) DI Balance GA (70%) 30° C. pH HCX32-0Br-p3 0.5 0 0 20 80 0.819 3.67 3.4 HCX32-Br005-p3 0.5 0.5 0 20 80 0.249 25.81 3.5 HCX32-Br03-p3 0.5 3 0 20 80 0.238 30.22 3.4 HCX32-Cl005-p3 0.5 0 0.5 20 80 0.263 22.51 3.4 HCX32-Cl03-p3 0.5 0 3 20 80 0.258 31.01 3.4

TABLE 5B Formulations and W etch rate at 30° C., pH 7 and pH 8.7 Formulation Process Temp (° C.) W (Å/min) HCX-T002C-32-P8 30 21.87 HCX-T002C-32-Br005-P8 56.18 HCX-T002C-32-Br03-P8 97.08 HCX-T002C-32-Cl005-P8 50.60 HCX-T002C-32-Cl03-P8 143.17 HCX-T002C-32-P7 7.11 HCX-T002C-32-Br005-P7 27.08 HCX-T002C-32-Br03-P7 31.62 HCX-T002C-32-Cl005-P7 28.80 HCX-T002C-32-Cl03-P7 36.78

The results are shown graphically in FIGS. 11, 12, 13 and 14 where it can be seen that for NH₄Cl and NH₄Br the etch rate for W metal hardmask increased as the concentration of halide anion increased from 0 to 0.3 wt % for the pH range of from acidic to basic.

Low-K Compatibility

The compositions shown in Table 6A, 6B & 6C were prepared and TEOS etch rate evaluations were carried out as described above at temperatures of 30° C. and 50° C., respectively.

TABLE 6A TEOS Etch Rate and NH₄Br Formulations at pH 7 Formulation and TEOS Etch Rate Component TEOS (30° C.) TEOS (50° C.) NH4Br H2O2 Etch Rate Etch Rate Formulation (10%) BTA Pyrazole DGA (10%) DI balance (30%) (Å/min) (Å/min) pH HCX-T002C-32B-BrCl0 0 0.8 0 0.2934 80 20 −0.13 0.42 7.1 HCX-T002C-32B-Br03 3 0.8 0 0.3134 80 20 0.17 0.16 7.0 HCX-T002C-32B-Br1 10 0.8 0 0.3288 80 20 0.22 0.36 7.0 HCX-T002C-32B-Br3 30 0.8 0 0.4166 80 20 0.08 0.17 7.0 HCX-T002C-32B-Br5 50 0.8 0 0.4336 80 20 0.05 0.21 7.0 HCX-T002C-32-Br0 0 0 0.5 0.0386 80 20 0.01 0.17 7.0 HCX-T002C-32-Br3 30 0 0.5 0.1749 80 20 0.15 0.21 7.0 HCX-T002C-32-Br5 50 0 0.5 0.3106 80 20 0 −0.07 7.0

TABLE 6B TEOS Etch Rate and NH₄Cl Formulations at pH 7 Formulation and TEOS Etch Rate Component TEOS (50° C.) NH4Cl H2O2 TEOS (30° C.) Etch Rate Formulation (10%) BTA Pyrazole DGA (10%) DI balance (30%) Etch Rate (Å/min) (Å/min) pH HCX-T002C-32B-Cl0 0 0.8 0 0.2934 80 20 −0.13 0.42 7.1 HCX-T002C-32B-Cl03 3 0.8 0 0.4396 80 20 −0.19 −0.10 7.2 HCX-T002C-32B-Cl1 10 0.8 0 0.4341 80 20 0.26 0.32 7.1 HCX-T002C-32B-Cl3 30 0.8 0 0.5082 80 20 0.19 0.30 7.0 HCX-T002C-32B-Cl5 50 0.8 0 0.5531 80 20 −0.54 0.32 7.0 HCX-T002C-32-Cl0 0 0 0.5 0.0386 80 20 0.01 0.17 7.0 HCX-T002C-32-Cl3 30 0 0.5 0.2611 80 20 0.05 0.14 7.0 HCX-T002C-32-Cl5 50 0 0.5 0.4751 80 20 0.11 0.07 7.1

TABLE 6C TEOS Etch Rate and NH₄F Formulations at pH 7 Formulation and TEOS Etch Rate Component TEOS (30° C.) TEOS (50° C.) DI H2O2 Etch Rate Etch Rate Formulation NH4F (10%) BTA Pyrazole DGA (10%) balance (30%) pH (Å/min) (Å/min) HCX-T002C-32B-F0 0 0.8 0 0.294 80 20 7 −0.13 0.42 HCX-T002C-32B-F03 3 0.8 0 0.389 80 20 7 −0.07 0.28 HCX-T002C-32B-F1 10 0.8 0 0.387 80 20 7 0.20 0.69 HCX-T002C-32B-F3 30 0.8 0 0.343 80 20 7 0.44 3.59 HCX-T002C-32B-F5 50 0.8 0 0.245 80 20 7 1.78 8.88 HCX-T002C-32-F0 0 0 0.5 0.031 80 20 7 0.01 0.69 HCX-T002C-32-F3 30 0 0.5 0.001 80 20 7 0.63 3.53 HCx-T002C-32-F5 50 0 0.5 0.000 80 20 7 1.45 8.99

TEOS etch rate results are shown graphically in FIGS. 15 and 16 where it can be seen that with the inclusion of NH₄Cl or NH₄Br the etch rate for TEOS remains insignificant as the concentration of halide anion increases from 0 to 5 wt %. In contrast, the TEOS etch rate increases as the concentration of NH₄F increases from 0 to 5 wt %. The results indicate that compositions which contain halide anion Cl⁻ or Br⁻ do not etch TEOS. Low-k materials consist of porious TEOS, and this result indicates that the formulations with NH₄Br (or NH₄Cl) are compatible with low-k materials.

Cleaning Performance

Wafers were processed as described above, and the cleaning performance results are shown in FIG. 17 which illustrates that etch residues are satisfactorily removed after chemical treatments at 30° C. for 90 seconds.

The compositions and method according to the inventive concepts described herein have excellent properties and are uniquely capable of selectively etching TiN, TiNxOy or W metal hardmasks, are compatible with Cu and low-k dielectric materials, and can also simultaneously remove copper oxide, polymeric materials and etch residues from the substrate being treated.

Formulations and Their Performance

The formulations below are designed for all applications where corrosion of copper components during semiconductor device manufacture is not a concern, and formulations prepared according to the inventive concepts described herein do not contain a corrosion inhibitor.

The compositions shown in Tables 7A and 7B were prepared and TEOS etch rate evaluations were carried out as described above at a temperature of 55′C. Table 7A shows TEOS etch rate data measured at pH=7, while Table 7B shows TEOS etch rate data measured at pH=8. The measured TEOS etch rates are summarized in Tables 7A and 7B and are shown graphically in FIGS. 18-21. It is seen from these graphs that the TEOS etch rate is not impacted by the level of either of the ammonium bromide or ammonium chloride level, but etch rate increases with increasing ammonium fluoride level.

The compositions shown in Tables 7C and 7D were prepared and TIN etch rate evaluations were carried out as described above at a temperature of 40′C. Table 7C shows TiN etch rate data measured at pH=7, while Table 7D shows TiN etch rate data measured at pH=8. The measured TiN etch rates are summarized in Tables 7C and 7D and are shown graphically in FIGS. 22-23. It is seen from these graphs that the TiN etch rate increases with increasing levels of ammonium bromide, ammonium chloride, and ammonium fluoride.

TABLE 7A TEOS Etch Rate at pH 7, 55° C. Component TEOS (55° C.) NH4Br NH4F NH4Cl DGA H2O2 Etch Rate Formulation (10%) (10%) (10%) (10%) DI balance (30%) pH (Å/min) HCX33-F0-7 0 0 0 0.023 80 20 7 0.09 HCX33-F10-7 0 10 0 0.027 80 20 7 1.22 HCX33-F30-7 0 30 0 0.000 80 20 7 5.61 HCX33-F50-7 0 50 0 0.000 80 20 7 12.06 HCX33-Br10-7 31.6 0 0 0.206 80 20 7 0.20 HCX33-Br30-7 94.7 0 0 0.532 80 20 7 0.19 HCX33-Br50-7 157.8 0 0 0.844 80 20 7 0.19 HCX33-Cl10-7 0 0 14.4 0.136 80 20 7 0.06 HCX33-Cl30-7 0 0 43.3 0.327 80 20 7 −0.01 HCX33-Cl50-7 0 0 72.2 0.461 80 20 7 0.07 *Formulations with Br and Cl in the designated name contain NH₄Br and NH₄Cl, respectively.

TABLE 7B TEOS Etch Rate at pH 8, 55° C. Component TEOS (55° C.) NH4Br NH4F NH4Cl DGA H2O2 Etch Rate Formulation (10%) (10%) (10%) (10%) DI balance (30%) pH (Å/min) HCX33-F0-8 0 0 0 0.017 80 20 8 0.13 HCX33-F10-8 0 10 0 0.100 80 20 8 1.17 HCX33-F30-8 0 30 0 0.204 80 20 8 2.69 HCX33-F50-8 0 50 0 0.294 80 20 8 4.54 HCX33-Br10-8 31.6 0 0 0.179 80 20 8 0.67 HCX33-Br30-8 94.7 0 0 0.417 80 20 8 0.79 HCX33-Br50-8 157.8 0 0 0.672 80 20 8 0.93 HCX33-Cl10-8 0 0 14.4 0.124 80 20 8 0.33 HCX33-Cl30-8 0 0 43.3 0.295 80 20 8 0.25 HCX33-Cl50-8 0 0 72.2 0.431 80 20 8 0.40 *Formulations with Br and Cl in the designated name contain NH₄Br and NH₄Cl, respectively.

TABLE 7C TiN Etch Rate at pH 7, 40° C. Component TiN (40° C.) NH4Br NH4Cl DI Etch Rate Formulation (10%) (10%) DGA (10%) balance H2O2 (30%) pH (Å/min) HCX33-Br0-7 0 0 0.036 80 20 7 8.59 HCX33-Br05-7 0.5 0 0.037 80 20 7 15.88 HCX33-Br3-7 3 0 0.052 80 20 7 21.11 HCX33-Br5-7 5 0 0.071 80 20 7 24.41 HCX33-Cl0-7 0 0 0.038 80 20 7 9.87 HCX33-Cl05-7 0 0.5 0.041 80 20 7 18.89 HCX33-Cl3-7 0 3 0.066 80 20 7 24.96 HCX33-Cl5-7 0 5 0.084 80 20 7 25.93 *Formulations with Br and Cl in the designated name contain NH₄Br and NH₄Cl, respectively.

TABLE 7D TiN Etch Rate at pH 8, 40° C. Component TiN (40° C.) NH4Br NH4Cl DI Etch Rate Formulation (10%) (10%) DGA (10%) balance H2O2 (30%) pH (Å/min) HCX33-Br0-8 0 0 0.134 80 20 8 19.30 HCX33-Br05-8 0.5 0 0.207 80 20 8 30.59 HCX33-Br3-8 3 0 0.335 80 20 8 36.28 HCX33-Br5-8 5 0 0.470 80 20 8 39.52 HCX33-Cl0-8 0 0 0.116 80 20 8 17.09 HCX33-Cl05-8 0 0.5 0.265 80 20 8 37.24 HCX33-Cl3-8 0 3 0.593 80 20 8 43.26 HCX33-Cl5-8 0 5 0.742 80 20 8 48.2 *Formulations with Br and Cl in the designated name contain NH₄Br and NH₄Cl, respectively. 

What is claimed is:
 1. A method for simultaneously removing polymeric materials and etch residues and selectively etching TiN or titanium oxynitride from a semiconductor device comprising Cu, low-k dielectric material and TiN or titanium oxynitride which comprises: contacting the semiconductor device with an aqueous composition comprising at least one halide anion selected from Cl— or Br—, and at least one oxidizing agent in the absence of a Cu corrosion inhibitor and wherein the composition is effective in removing polymeric materials and etch residues and selectively etching TiN or titanium oxynitride from a semiconductor device comprising Cu, low-k dielectric material and TiN or titanium oxynitride, and wherein the composition has a pH of at least 7.0 or higher.
 2. The method of claim 1 wherein the composition includes a hydroxide source.
 3. The method of claim 1 wherein the temperature is in the range of from 20° C. to about 60° C. and the oxidizing agent is selected from the group consisting of hydrogen peroxide, ozone, ferric chloride, permanganate, peroxoborate, perchlorate, persulfate, ammonium peroxydisulfate, per acetic acid, urea hydroperoxide, percarbonate, perborate, and mixtures thereof.
 4. The method of claim 1 wherein the composition further comprising an organic cosolvent that is miscible with water.
 5. The method of claim 1 wherein the composition is effective in removing etch residues.
 6. The method of claim 1 wherein the composition is effective in selectively etching TiN or titanium oxynitride from a semiconductor device comprising Cu, low-k dielectric material and TiN or titanium oxynitride. 